EP0343735A3 - Process for partial oxidation of a liquid or solid and/or a gaseous hydrocarbon-containing fuel - Google Patents

Process for partial oxidation of a liquid or solid and/or a gaseous hydrocarbon-containing fuel Download PDF

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Publication number
EP0343735A3
EP0343735A3 EP19890201292 EP89201292A EP0343735A3 EP 0343735 A3 EP0343735 A3 EP 0343735A3 EP 19890201292 EP19890201292 EP 19890201292 EP 89201292 A EP89201292 A EP 89201292A EP 0343735 A3 EP0343735 A3 EP 0343735A3
Authority
EP
European Patent Office
Prior art keywords
liquid
solid
channel
concentric
partial oxidation
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
EP19890201292
Other languages
German (de)
French (fr)
Other versions
EP0343735A2 (en
EP0343735B1 (en
Inventor
Franciscus Johanna Arnoldus Martens
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Shell Internationale Research Maatschappij BV
Original Assignee
Shell Internationale Research Maatschappij BV
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority claimed from GB888812472A external-priority patent/GB8812472D0/en
Application filed by Shell Internationale Research Maatschappij BV filed Critical Shell Internationale Research Maatschappij BV
Publication of EP0343735A2 publication Critical patent/EP0343735A2/en
Publication of EP0343735A3 publication Critical patent/EP0343735A3/en
Application granted granted Critical
Publication of EP0343735B1 publication Critical patent/EP0343735B1/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/32—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
    • C01B3/34—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
    • C01B3/36—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using oxygen or mixtures containing oxygen as gasifying agents
    • C01B3/363—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using oxygen or mixtures containing oxygen as gasifying agents characterised by the burner used

Abstract

Process for the partial oxidation of a liquid or solid and/or a gaseous fuel using a multi-orifice burner comprising a central channel and four concentric channels encircling the central channel. Liquid or solid fuel is supplied through the second concentric channel and the oxidizer is supplied through the first concentric channel and the third concentric channel. Hydrocarbon gas and/or moderator is supplied through the central channel and the fourth concentric channel. The supplies occur at specific mass flow distributions and velocities. The mass ratio of liquid or solid fuel to hydrocarbon gas ranges from 0 to 1.
EP89201292A 1988-05-26 1989-05-19 Process for partial oxidation of a liquid or solid and/or a gaseous hydrocarbon-containing fuel Expired - Lifetime EP0343735B1 (en)

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
GB888812472A GB8812472D0 (en) 1988-05-26 1988-05-26 Process for simultaneous partial oxidation liquid/solid & gaseous hydrocarbon-containing fuel
GB8812472 1988-05-26
GB8822946 1988-09-30
GB8822946A GB2219003A (en) 1988-05-26 1988-09-30 Process for partial oxidation of a liquid or solid and/or gaseous hydrocarbon-containing fuel

Publications (3)

Publication Number Publication Date
EP0343735A2 EP0343735A2 (en) 1989-11-29
EP0343735A3 true EP0343735A3 (en) 1991-10-09
EP0343735B1 EP0343735B1 (en) 1996-04-10

Family

ID=26293934

Family Applications (1)

Application Number Title Priority Date Filing Date
EP89201292A Expired - Lifetime EP0343735B1 (en) 1988-05-26 1989-05-19 Process for partial oxidation of a liquid or solid and/or a gaseous hydrocarbon-containing fuel

Country Status (12)

Country Link
US (1) US4888031A (en)
EP (1) EP0343735B1 (en)
JP (1) JP2640979B2 (en)
CN (1) CN1015251B (en)
AT (1) ATE136525T1 (en)
AU (1) AU611803B2 (en)
CA (1) CA1321878C (en)
DE (1) DE68926180T2 (en)
ES (1) ES2085859T3 (en)
MY (1) MY104022A (en)
NO (1) NO892081L (en)
PT (1) PT90650B (en)

Families Citing this family (33)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5087271A (en) * 1990-11-19 1992-02-11 Texaco Inc. Partial oxidation process
DE69503781T2 (en) * 1994-05-19 1999-02-11 Shell Int Research METHOD FOR PRODUCING SYNTHESIS GAS BY PARTIAL OXIDATION OF THE LIQUID HYDROCARBON LIQUID, WHICH A BURNER WITH MULTIPLE (CONCENTRIC, RING-SHAPED) EXHAUST OPENINGS IS USED
AU696238B2 (en) * 1994-07-07 1998-09-03 Shell Internationale Research Maatschappij B.V. Process for the preparation of hydrogen and carbon monoxide containing mixtures
MY115440A (en) * 1994-07-22 2003-06-30 Shell Int Research A process for the manufacture of synthesis gas by partial oxidation of a gaseous hydrocarbon-containing fuel using a multi-orifice (co-annular)burner
US5688115A (en) * 1995-06-19 1997-11-18 Shell Oil Company System and method for reduced NOx combustion
US5931978A (en) * 1995-12-18 1999-08-03 Shell Oil Company Process for preparing synthesis gas
US5866620A (en) * 1996-08-08 1999-02-02 Shell Oil Company Process for carrying out an exothermic reaction
US6126908A (en) * 1996-08-26 2000-10-03 Arthur D. Little, Inc. Method and apparatus for converting hydrocarbon fuel into hydrogen gas and carbon dioxide
US6245303B1 (en) 1998-01-14 2001-06-12 Arthur D. Little, Inc. Reactor for producing hydrogen from hydrocarbon fuels
US6269286B1 (en) * 1998-09-17 2001-07-31 Texaco Inc. System and method for integrated gasification control
US6641625B1 (en) 1999-05-03 2003-11-04 Nuvera Fuel Cells, Inc. Integrated hydrocarbon reforming system and controls
US6892654B2 (en) * 2002-04-18 2005-05-17 Eastman Chemical Company Coal gasification feed injector shield with oxidation-resistant insert
US6755355B2 (en) 2002-04-18 2004-06-29 Eastman Chemical Company Coal gasification feed injector shield with integral corrosion barrier
ITMI20041860A1 (en) * 2004-09-30 2004-12-30 Eni Spa EQUIPMENT TO SPRAY A LIQUID CURRENT WITH A GASEY DISPERSING CURRENT AND MIX THE NEBULIZED PRODUCT WITH AN ADDITIONAL GASEOUS CURRENT SUITABLE FOR EQUIPMENT TO CARRY OUT PARTIAL CATALYTIC OXIDATIONS AND ITS PROCEEDS
MY145373A (en) * 2006-07-11 2012-01-31 Shell Int Research Process to prepare a synthesis gas
MY148270A (en) * 2006-07-14 2013-03-29 Shell Int Research A process for the manufacture of synthesis gas by partial oxidation of a liquid hydrocarbon-containing fuel using a multi-orifice burner
US20090272822A1 (en) * 2008-04-30 2009-11-05 General Electric Company Feed injector systems and methods
JP5115372B2 (en) * 2008-07-11 2013-01-09 トヨタ自動車株式会社 Operation control device for gas turbine
US8349046B2 (en) * 2009-04-30 2013-01-08 Enerjetik Llc Method of making syngas and apparatus therefor
US8360342B2 (en) 2010-04-30 2013-01-29 General Electric Company Fuel injector having differential tip cooling system and method
US9079199B2 (en) 2010-06-14 2015-07-14 General Electric Company System for increasing the life of fuel injectors
US9033033B2 (en) 2010-12-21 2015-05-19 Chevron U.S.A. Inc. Electrokinetic enhanced hydrocarbon recovery from oil shale
CA2822659A1 (en) 2010-12-22 2012-06-28 Chevron U.S.A. Inc. In-situ kerogen conversion and recovery
US9941025B2 (en) * 2011-04-08 2018-04-10 Terrapower, Llc Nuclear fuel and method of fabricating the same
CN104254489B (en) 2011-10-18 2017-09-15 国际壳牌研究有限公司 The production of synthesis gas
US8851177B2 (en) 2011-12-22 2014-10-07 Chevron U.S.A. Inc. In-situ kerogen conversion and oxidant regeneration
US8701788B2 (en) 2011-12-22 2014-04-22 Chevron U.S.A. Inc. Preconditioning a subsurface shale formation by removing extractible organics
US9181467B2 (en) 2011-12-22 2015-11-10 Uchicago Argonne, Llc Preparation and use of nano-catalysts for in-situ reaction with kerogen
US8992771B2 (en) 2012-05-25 2015-03-31 Chevron U.S.A. Inc. Isolating lubricating oils from subsurface shale formations
WO2022171906A2 (en) 2021-04-28 2022-08-18 Torrgas Technology B.V. Process to prepare lower olefins
EP4116623A1 (en) 2021-07-05 2023-01-11 Linde GmbH Burner for performing partial oxidation
EP4163545A1 (en) 2021-10-07 2023-04-12 Linde GmbH Burner for performing partial oxidation
EP4163546A1 (en) 2021-10-07 2023-04-12 Linde GmbH Device and method for performing partial oxidation

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0098043A2 (en) * 1982-06-29 1984-01-11 Texaco Development Corporation Partial oxidation burner and process
EP0255748A2 (en) * 1986-08-05 1988-02-10 Shell Internationale Researchmaatschappij B.V. Process for partial oxidation of a hydrocarbon-containing fuel

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3840355A (en) * 1972-06-28 1974-10-08 Texaco Inc Partial oxidation of hydrocarbons to synthesis gas
US4351647A (en) * 1980-07-14 1982-09-28 Texaco Inc. Partial oxidation process
US4491456A (en) * 1982-06-29 1985-01-01 Texaco Inc. Partial oxidation process
US4502633A (en) * 1982-11-05 1985-03-05 Eastman Kodak Company Variable capacity gasification burner
US4443230A (en) * 1983-05-31 1984-04-17 Texaco Inc. Partial oxidation process for slurries of solid fuel
GB2164951A (en) * 1984-09-26 1986-04-03 Shell Int Research Method and apparatus for producing synthesis gas

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0098043A2 (en) * 1982-06-29 1984-01-11 Texaco Development Corporation Partial oxidation burner and process
EP0255748A2 (en) * 1986-08-05 1988-02-10 Shell Internationale Researchmaatschappij B.V. Process for partial oxidation of a hydrocarbon-containing fuel

Also Published As

Publication number Publication date
AU3514089A (en) 1989-11-30
EP0343735A2 (en) 1989-11-29
CN1015251B (en) 1992-01-01
CA1321878C (en) 1993-09-07
CN1038069A (en) 1989-12-20
MY104022A (en) 1993-10-30
EP0343735B1 (en) 1996-04-10
NO892081D0 (en) 1989-05-24
JPH0243288A (en) 1990-02-13
US4888031A (en) 1989-12-19
ATE136525T1 (en) 1996-04-15
PT90650B (en) 1994-10-31
DE68926180T2 (en) 1996-08-29
JP2640979B2 (en) 1997-08-13
DE68926180D1 (en) 1996-05-15
AU611803B2 (en) 1991-06-20
PT90650A (en) 1989-11-30
ES2085859T3 (en) 1996-06-16
NO892081L (en) 1989-11-27

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